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Removing Contaminants From Crude Oil

a technology of crude oil and contaminants, applied in the direction of hydrocarbon oil dewatering/demulsification, refining by water treatment, instruments, etc., can solve the problems of restricting the use of specific water-soluble hydroxyacids in desalting operations, affecting the quality of crude oil, and amines are common unwanted contaminants. , to achieve the effect of reducing over-acidification

Active Publication Date: 2018-03-22
BP CORP NORTH AMERICA INC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

The present invention is based on the discovery that the pH of an aqueous phase affects the amount of contaminants that can be removed from crude oil. By controlling the pH, the amount of acid or base used to control the pH, and the nature of the acid or base, contaminants can be effectively removed from the oil without over-acidification. This optimisation of a partitioning process forms the basis of the invention.

Problems solved by technology

Amines are a common unwanted contaminant.
Movement of the acids into the crude oil phase in this way can itself lead to problems with refinery apparatus downstream of the desalter.
However, the use of specific water-soluble hydroxyacids in a commercial desalting operation can turn out to be expensive and restricting, e.g. as compared to methods in which commodity acids may be used.
Accordingly, the use of correlations between ambient pH and partitioning in selecting conditions for a commercial desalting process may be of limited benefit.

Method used

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  • Removing Contaminants From Crude Oil
  • Removing Contaminants From Crude Oil
  • Removing Contaminants From Crude Oil

Examples

Experimental program
Comparison scheme
Effect test

example 1

ng Partitioning Levels of Amine Contaminants with Process pH

[0099]Partitioning levels for the amines monomethylamine (MMA), monoethanolamine (MEA) and ammonia (NH3) were measured across a range of pH levels at process conditions. A number of different acids were used to control the pH in the experiments. Further additives were also introduced into the system (such as further bases and metal salts) to investigate whether the presence of different types of additive may have an effect on the correlation between amine partitioning levels and process pH. Graphs depicting the correlations are shown in FIGS. 1a-c.

[0100]It can be seen that there is a strong correlation between amine partitioning level and the pH of the aqueous phase at process conditions, with higher partitioning levels observed at lower aqueous phase pH. It can also be seen that the correlation is substantially independent of the acid, or mixture of acids, being used. Furthermore, the correlation is not impacted by the pr...

example 2

ng Partitioning Levels of Acids of Interest with Process pH

[0101]Partitioning levels for the acids acetic acid (AcOH), hydrochloric acid (HC), citric acid, glycolic acid, malic acid, maleic acid, and H2S were measured across a range of pH levels. A number of different bases were used to control the pH in the experiments. Further additives were also introduced into the system (such as further acids and metal salts) to investigate whether the presence of different types of additive may have an effect on the correlation between acid partitioning levels and process pH. Graphs depicting the correlations are shown in FIGS. 2a-g.

[0102]A strong correlation between acid partitioning levels and the pH of the aqueous phase at process conditions was observed, with lower partitioning levels observed at lower aqueous phase pH. As with amine contaminants, the results indicate that the inclusion of further additives in the system does not impact on the correlation.

example 3

Acidic Conditions for Use in a Partitioning Process

[0103]Correlations between the partitioning levels and the pH of the aqueous phase for monoethanolamine were plotted against correlations between the partitioning levels and the pH of the aqueous phase for six different acids of interest: acetic acid, glycolic acid, maleic acid, malic acid, citric acid and hydrochloric acid. Graphs depicting the correlations are shown in FIGS. 3a-f.

[0104]It can be seen from the graphs that approximately 99% of monoethanolamine was partitioned into the aqueous phase at pH levels of 5 or below. However, only some of the acids of interests achieve a partitioning level of greater 80% into the aqueous phase at pH levels of 5 or below. For instance, it can be seen from FIG. 3a that approximately 70% of the acetic acid remained in the non-aqueous phase at pH levels of 5 or below. This level of acid in the non-aqueous phase is clearly undesirable, since it will lead to corrosion downstream in a refinery. A...

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PUM

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Abstract

A method comprises correlating—in a system which comprises a non-aqueous phase comprising a hydrocarbon fluid, and an aqueous phase—partitioning levels of a basic contaminant and / or an acid of interest into the aqueous phase with the pH of the aqueous phase. The partitioning levels of the basic contaminant and the acid of interest, as well as the pH of the aqueous phase, are obtained under conditions which are representative of those used in a partitioning process in which a basic contaminant is removed from a hydrocarbon fluid.The correlations may be used in a method for selecting an acidic environment for use in a partitioning process, for estimating corrosion risk downstream of a partitioning process, or for controlling a partitioning process.

Description

FIELD OF THE INVENTION[0001]The present invention relates to a method for correlating partitioning levels of a basic contaminant and / or an acid of interest from a hydrocarbon fluid with pH. The correlations may be used in a method for selecting an acidic environment for use in a partitioning process in which a basic contaminant is partitioned from a hydrocarbon fluid into an aqueous phase. The present invention is of particular use in crude oil desalting operations, since it enables basic contaminants, such as ammonia, organic amines and metal salts, to be removed during a desalting operation without unnecessary over-acidification of the crude oil.BACKGROUND OF THE INVENTION[0002]Crude oil contains a number of contaminants which are desirably removed before the crude oil is processed. Amines are a common unwanted contaminant.[0003]Amines may make their way into a crude oil for a number of reasons. One common reason is due to the use of nitrogen-containing compounds in removing hydro...

Claims

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Application Information

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IPC IPC(8): C10G17/04C10G17/06G01N33/28
CPCC10G17/04C10G17/06G01N33/2823G01N33/2876C10G2300/202C10G31/08C10G33/00C10G17/00C10G21/06
Inventor ZHOU, CHENGXIANGWEI, MINGENGLISH, JASONHACKETT, CRAIG
Owner BP CORP NORTH AMERICA INC